首页> 外国专利> PROCESS FOR CONVERTING METHANOL TO ALKYL ETHERS, GASOLINE, DISTILLATE, AND ALKYLATE LIQUID HYDROCARBONS

PROCESS FOR CONVERTING METHANOL TO ALKYL ETHERS, GASOLINE, DISTILLATE, AND ALKYLATE LIQUID HYDROCARBONS

机译:甲醇转化为烷基醚,汽油,蒸馏水和烷基化液态烃的过程

摘要

A MULTISTAGE PROCESS FOR PRODUCING ISOALKYL ETHERS FROM LOWER ALIPHATIC OXYGENATE FEEDSTOCK, SUCH AS METHANOL. FEEDSTOCK IS CATALYTICALLY CONVERTED IN A PRIMARY CATALYST STAGE AT ELEVATED TEMPERATURE IN CONTACT WITH ZEOLITE CATALYST TO PREDOMINANTLY C2-C7 LOWER OLEFINS COMPRISING ISOBUTYLENE AND ISOAMYLENE, BY-PRODUCT WATER AND A MINOR AMOUNT OF C8+ HYDROCARBONS, FOLLOWED BY FRACTIONATION OF THE C2-C7 OLEFINS TO RECOVER A C2-C3-RICH RECYCLE STREAM FOR FURTHER CATALYTIC CONVERSION IN THE PRIMARY STAGE. C4-C7 OLEFINS ARE PASSED TO A SECOND CATALYTIC ETHERIFICATION STAGE FOR REACTION OF ISOALKENES WITH METHANOL TO PRODUCE METHYL TERTIARY-BUTYL ETHER, METHYL ISOAMYLETHER AND HIGHER ISOALKYL ETHERS.THE SECOND STAGE EFFLUENT MAY BE FRACTIONATED TO RECOVER AN ETHER PRODUCT, C5+ HYDROCARBON LIQUID PRODUCT, AND UNREACTED BUTENES. ADVANTAGEOUSLY, THE UNREACTED BUTENES ARE FURTHER REACTED WITH ISOPARAFFIN IN A THIRD CATALYST STAGE UNDER ACID CATALYSIS ALKYLATION CONDITIONS, AND FRACTIONATED TO RECOVER C6+ ALKYLATE LIQUID, LIQUID HYDROCARBON PRODUCT. THE ETHERS MAY BE BLENDED WITH AT LEAST ONE C6+ HYDROCARBON TO PRODUCE HIGH OCTANE GASOLINE.
机译:从低级含氧汽油中(如甲醇)生产异烷基醚的多步工艺。在升高的温度下,与沸石催化剂接触,在主催化剂阶段将催化转化为主要转化为C2-C7的低级烯烃,主要由异丁烯和异戊烯,副产物水和少量的C7 +馏分通过水生成的C7 +恢复富含C2-C3的循环流,以在主要阶段进一步进行催化转化。将C4-C7烯烃传递至第二催化醚化阶段,以使异烯烃与甲醇反应生成甲基叔丁基醚,甲基异戊二烯和更高的异烷基乙基醚。第二步产物可能会连续多次反应和未完成的丁字裤。有利地,未反应的丁二酸酯在酸性催化烷基化条件下的第三催化剂阶段进一步与异链烷烃反应,并经分馏以回收C6 +烷基化液态,液态烃产品。可能会混合至少一种C6 +烃,以生产高辛烷汽油。

著录项

  • 公开/公告号MY101759A

    专利类型

  • 公开/公告日1992-01-17

    原文格式PDF

  • 申请/专利权人

    申请/专利号MYPI 87001033

  • 申请日1987-07-16

  • 分类号C07C1/20;C07C2/00;

  • 国家 MY

  • 入库时间 2022-08-22 05:34:04

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